JPH0780970B2 - Method for manufacturing water-absorbent composite material - Google Patents

Method for manufacturing water-absorbent composite material

Info

Publication number
JPH0780970B2
JPH0780970B2 JP61201354A JP20135486A JPH0780970B2 JP H0780970 B2 JPH0780970 B2 JP H0780970B2 JP 61201354 A JP61201354 A JP 61201354A JP 20135486 A JP20135486 A JP 20135486A JP H0780970 B2 JPH0780970 B2 JP H0780970B2
Authority
JP
Japan
Prior art keywords
water
fibrous substrate
monomer
polymerizable monomer
aqueous solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61201354A
Other languages
Japanese (ja)
Other versions
JPS6357617A (en
Inventor
喜一 伊藤
毅 芝野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP61201354A priority Critical patent/JPH0780970B2/en
Priority to US07/088,277 priority patent/US4865886A/en
Priority to TW076105007A priority patent/TW255900B/zh
Priority to EP87112486A priority patent/EP0262405B1/en
Priority to ES198787112486T priority patent/ES2027267T3/en
Priority to DE8787112486T priority patent/DE3774232D1/en
Priority to AU77661/87A priority patent/AU600024B2/en
Priority to KR1019870009468A priority patent/KR950013035B1/en
Priority to CA000545646A priority patent/CA1302806C/en
Publication of JPS6357617A publication Critical patent/JPS6357617A/en
Publication of JPH0780970B2 publication Critical patent/JPH0780970B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M14/00Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials
    • D06M14/02Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin
    • D06M14/04Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin of vegetal origin, e.g. cellulose or derivatives thereof
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M14/00Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials
    • D06M14/08Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of synthetic origin
    • D06M14/12Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of synthetic origin of macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • D06M14/14Polyesters

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Absorbent Articles And Supports Therefor (AREA)
  • Polymerisation Methods In General (AREA)
  • Treatments Of Macromolecular Shaped Articles (AREA)
  • Reinforced Plastic Materials (AREA)
  • Graft Or Block Polymers (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Description

【発明の詳細な説明】 〔発明の背景〕 産業上の利用分野 本発明は、吸水性ポリマーと成形した繊維質基体とから
なる吸水性複合材料の製造法に関するものである。更に
詳しくは、本発明は、アクリル酸系モノマー水溶液を成
形した繊維質基体に施し、このモノマーを重合させて複
合体前駆体をつくり、これを更に架橋させることからな
る、高吸水性ポリマーが成形した繊維質基体に固定され
た吸水性複合材料の製造法に関するものである。
Description: BACKGROUND OF THE INVENTION Field of the Invention The present invention relates to a method for producing a water-absorbing composite material comprising a water-absorbing polymer and a molded fibrous substrate. More specifically, the present invention provides a highly water-absorbing polymer formed by applying an aqueous acrylic acid-based monomer solution to a molded fibrous substrate, polymerizing the monomer to form a composite precursor, and further crosslinking the composite precursor. The present invention relates to a method for producing a water-absorbent composite material fixed to a fibrous base material.

本発明の製造法で得られる吸水性複合材料は、吸水性に
優れ、しかも高吸水性ポリマーが繊維質基体に安定性良
く固定されているので、各種の吸水性材料の製造に有利
に使用することができる。
The water-absorbent composite material obtained by the production method of the present invention is excellent in water absorbency, and since the superabsorbent polymer is fixed to the fibrous substrate with good stability, it is advantageously used for production of various water-absorbent materials. be able to.

従来技術 従来、紙、パルプ、不織布、スポンジ状ウレタン樹脂等
は、保水剤として生理用ナプキン、紙オシメ等を始めと
する各種の衛生材料及び各種の農業用材料等として使用
されてきた。しかし、これらの材料はその吸水量が自重
の10〜50倍程度に過ぎないので、多量の水を吸収又は保
持させるためには多量の材料が必要であって、著しく嵩
高になるばかりでなく、また吸水した材料を加圧すると
簡単に水分を放出する等の欠点があった。
2. Description of the Related Art Conventionally, paper, pulp, non-woven fabric, sponge-like urethane resin, etc. have been used as various water-retaining agents such as sanitary napkins, various kinds of sanitary materials such as paper naps, and various agricultural materials. However, since the water absorption amount of these materials is only about 10 to 50 times their own weight, a large amount of material is required to absorb or retain a large amount of water, and not only becomes extremely bulky, In addition, there is a drawback in that moisture is easily released when the water-absorbed material is pressurized.

この種の吸水材料の上記欠点を改善するものとして、近
年、高吸水性の種々の高分子材料が提案されている。例
えば、澱粉のグラフト重合体(特公昭53-46199号公報
等)、セルロース変性体(特開昭50-80376号公報等)、
水溶性高分子の架橋物(特公昭43-23462号公報等)、自
己架橋型アクリル酸アルカリ金属塩ポリマー(特公昭54
-30710号公報等)等が提案された。
In order to improve the above-mentioned drawbacks of this type of water absorbing material, various high water absorbing polymer materials have been proposed in recent years. For example, starch graft polymer (Japanese Patent Publication No. 53-46199, etc.), modified cellulose (Japanese Patent Publication No. 50-80376, etc.),
Crosslinked water-soluble polymer (Japanese Patent Publication No. 43-23462, etc.), self-crosslinking alkali metal acrylate polymer (Japanese Patent Publication No. 54
-30710, etc.) was proposed.

しかしながら、これらの高吸水性高分子材料は、その吸
水性能はかなりの高いレベルを有するものの、殆んどが
粉末状として得られるために、例えば生理用ナプキン、
紙オシメ等の衛生材料と使用するにはティシュ、不織
布、綿等の基材上に均一状に分散させる必要がある。し
かしながら、そのような方法で分散させたポリマー粉末
は基材上に安定良く固定することが困難であって、分散
後に一部局所に集合化することが多く、また吸水後の膨
潤ゲルを安定良く基材上に固定されずに基材から容易に
移動してしまう。このために、これを例えば紙オシメに
使用したとき、放尿後の吸水体は「ごわごわ」した状態
となり、極めて着用感の悪いものとなってしまう。ま
た、上記の様な粉末状ポリマーを基材に分散させて吸収
体を得る方法では、粉末の取扱いに伴う煩雑さおよび均
一な分散を効率良く行う上でのプロセス上の問題等によ
り、コスト的にも極めて割高になっている。
However, although these water-absorbent polymer materials have a considerably high level of water-absorbing performance, most of them are obtained in the form of powder, and therefore, for example, sanitary napkins,
In order to use it as a sanitary material such as a paper sheet, it is necessary to uniformly disperse it on a substrate such as tissue, non-woven fabric or cotton. However, it is difficult to stably fix the polymer powder dispersed by such a method on the base material, and it is likely that the polymer powder partially aggregates after the dispersion, and the swollen gel after water absorption is stable. It is not fixed on the base material and easily moves from the base material. For this reason, when this is used, for example, in a paper squeeze, the water absorbent body after urination becomes a "stiff" state, which makes it extremely uncomfortable to wear. In addition, the method of obtaining the absorbent body by dispersing the powdery polymer as described above in the substrate is costly because of the complexity involved in handling the powder and the process problems in efficiently performing uniform dispersion. It is extremely expensive.

これらの問題を解決する一つの方法として、アクリル酸
系モノマー水溶液を成形した繊維質基体に予め決めた模
様状に施した複合体を製造し、これに電磁放射線又は微
粒子性イオン化放射線を照射して、アクリル酸系モノマ
ーを高吸水性ポリマーに転換させて吸水性複合体を製造
する方法が報告されている(特公表57-500546号公
報)。この方法によれば、上記の粉体を取扱う上での均
一な分散化及び基材上への安定した固定化の点ではかな
りの改良がみられるものの、高吸水性ポリマーに転換す
るに当って、電磁放射線又は微粒子性イオン化放射線を
使用する為に、この特定のモノマーに生得的な高吸水性
のポリマーが過度に架橋化反応を受け易く、その結果、
得られる複合体は吸収体としての性能、特に吸水能、が
著しく小さく、通常前記粉末状高吸水性ポリマーを使用
した場合に比べて半分以下となってしまう欠点があるよ
うに思われる。
As one method for solving these problems, a composite obtained by applying an acrylic acid-based monomer aqueous solution to a fibrous substrate molded in a predetermined pattern is produced, and then irradiated with electromagnetic radiation or particulate ionizing radiation. , A method of producing a water-absorbing complex by converting an acrylic acid-based monomer into a super-water-absorbing polymer has been reported (Japanese Patent Publication No. 57-500546). According to this method, although there is a considerable improvement in terms of uniform dispersion in handling the above powder and stable immobilization on the substrate, in converting to a super absorbent polymer, Due to the use of electromagnetic radiation or particulate ionizing radiation, the superabsorbent polymer inherent in this particular monomer is too susceptible to cross-linking reactions, resulting in
The obtained composite has a remarkably small performance as an absorber, especially a water absorption capacity, and it seems that there is a drawback that it is usually less than half that in the case where the powdery superabsorbent polymer is used.

また、最近、特開昭60-149609号公報には、アクリル酸
塩系モノマー水溶液を予め吸水性有機材料に含浸させた
後、水溶性ラジカル重合開始剤又は水溶剤ラジカル重合
開始剤と水溶性還元剤を霧状にして添加して重合させる
吸水性複合材料の製造法が提案されている。しかしなが
ら、この方法では、アクリル酸系モノマーを吸水性有機
材料に含浸させた後、水溶性重合開始剤を添加するた
め、たとえ重合開始剤を霧状にしても「重合むら」が起
って、モノマーを完全に重合させることは極めて難かし
く、その結果、残存モノマーが多量となっており、安全
上問題が多く又性能的にも特に吸水能において小さくな
る等の欠点があるように思われる。
Further, recently, in JP-A-60-149609, a water-soluble radical polymerization initiator or a water-soluble radical polymerization initiator and a water-soluble reduction agent are prepared by impregnating a water-absorbing organic material with an aqueous solution of an acrylate-based monomer in advance. There has been proposed a method for producing a water-absorbing composite material in which the agent is atomized, added and polymerized. However, in this method, since the water-soluble polymerization initiator is added after the water-absorbing organic material is impregnated with the acrylic acid-based monomer, “polymerization unevenness” occurs even if the polymerization initiator is atomized, It is extremely difficult to completely polymerize the monomer, and as a result, the amount of residual monomer is large, and there are many safety problems, and it seems that there are drawbacks in terms of performance, especially in water absorption.

考えられる解決策 このような背景下、本発明者等は既に特願昭60-193403
号において、25重量%以上のモノマー濃度を有するアク
リル酸系モノマー水溶液と水溶性ラジカル重合開始剤あ
るいは水溶性ラジカル重合開始剤と水溶性還元剤を予め
均一混合後、繊維質基体中の高吸水性ポリマー粒子径が
30〜500μmとなる様に該混合液を霧状にして成形した
繊維質基体に施し、次いで重合させる方法を、特願昭60
-202908号において少量の架橋剤を含むアクリル酸系モ
ノマーの水溶液と水溶性ラジカル重合開始剤あるいは水
溶性ラジカル重合開始剤と水溶性還元剤を予め均一混合
後、繊維質基体中の高吸水性ポリマー粒子径が30〜500
μmとなる様に該混合液を霧状にして成形した繊維質基
体に施し、次いで重合させる方法を、特願昭60-238421
号において少量の架橋剤を含むアクリル酸系モノマーの
水溶液と酸化性のラジカル重合開始剤を混合後、繊維質
基体に施し、しかる後にアミン類又は還元剤を施して重
合させる方法を、さらに特願昭60-238420号において少
量の架橋剤を含むアクリル酸系モノマーの水溶液とアミ
ン類又は還元剤を混合後、繊維質基体を施し、しかる後
に酸化性ラジカル重合開始剤を施して重合させる方法、
等々を提案した。
Possible Solution Against this background, the present inventors have already filed Japanese Patent Application No. 60-193403.
No. 25, the aqueous solution of an acrylic acid-based monomer having a monomer concentration of 25% by weight or more and a water-soluble radical polymerization initiator or a water-soluble radical polymerization initiator and a water-soluble reducing agent are uniformly mixed in advance, and a high water absorption property in the fibrous substrate Polymer particle size
A method of applying the mixture to a fibrous substrate formed by atomizing the mixture so as to have a particle size of 30 to 500 μm, and then polymerizing the mixture is disclosed in Japanese Patent Application No.
-202908, a highly water-absorbent polymer in a fibrous substrate after previously uniformly mixing an aqueous solution of an acrylic acid monomer containing a small amount of a crosslinking agent and a water-soluble radical polymerization initiator or a water-soluble radical polymerization initiator and a water-soluble reducing agent. Particle size 30-500
A method of applying the mixture to a fibrous substrate formed into a mist so as to have a size of μm and then polymerizing the mixture is disclosed in Japanese Patent Application No. 60-238421.
Japanese Patent Application No. 2003-242242, a method of mixing an aqueous solution of an acrylic acid monomer containing a small amount of a cross-linking agent and an oxidizable radical polymerization initiator, and then applying to a fibrous substrate, and then applying an amine or a reducing agent to perform polymerization. After mixing an aqueous solution of an acrylic acid monomer containing a small amount of a cross-linking agent and an amine or a reducing agent in JP 60-238420 A, a fibrous substrate is applied, and then an oxidizing radical polymerization initiator is applied to perform polymerization.
And so on.

これらの方法では、前記のような粉体を取扱う上での均
一な分散化および基剤上への安定固着の点ではかなり改
善されるものの吸水速度が未だ小さく、特に生理用ナプ
キン、紙オシメ等の衛生材料に使用する場合の問題とな
っていた。
These methods are considerably improved in terms of uniform dispersion in handling the powder as described above and stable fixation on the base material, but the water absorption rate is still small, and especially sanitary napkins, paper naps, etc. It was a problem when used as a sanitary material.

〔発明の概要〕[Outline of Invention]

発明の目的 本発明は、前記特公表57-500546号公報および特開昭60-
149609号公報、に記載され、また本発明者らが特願昭60
-193403号、特願昭60-202908号、特願昭60-238421号、
および特願昭60-238420号において提案した吸水性複合
体をさらに改良して、吸水性能が大きく、特に吸水速度
が特段に大きな吸水性複合材料を温和な条件下で極めて
容易に製造する方法を提供しようとするものである。
OBJECT OF THE INVENTION The present invention includes the above-mentioned Japanese Patent Publication No. 57-500546 and JP-A-60-
Japanese Patent Application No.
-193403, Japanese Patent Application No. 60-202908, Japanese Patent Application No. 60-238421,
And a method of further improving the water-absorbing composite proposed in Japanese Patent Application No. 60-238420 to produce a water-absorbing composite having a large water-absorbing performance, particularly a particularly large water-absorbing speed under mild conditions. It is the one we are trying to provide.

発明の構成 本発明者等は、前記の問題点を解決する目的で種々研究
を重ねた結果、アクリル酸系モノマー水溶液を成形した
繊維質基体に施し、該アクリル酸系モノマーを重合さ
せ、しかる後にカルボキシル基および(または)カルボ
キシレート基で架橋させることにより、吸水性能が大き
く、特に吸水速度が特段に大きく、しかも高吸水性ポリ
マーが繊維質基体に安定性良く固定された吸水性複合材
料が極めて容易にかつ安価に得られることを見出して本
発明に到達した。
The present inventors have conducted various studies for the purpose of solving the above-mentioned problems, and as a result, applied an acrylic acid-based monomer aqueous solution to a molded fibrous substrate, polymerize the acrylic acid-based monomer, and then, By cross-linking with a carboxyl group and / or a carboxylate group, a water-absorbing composite material having a large water-absorbing performance, particularly a particularly high water-absorbing rate, and a highly water-absorbing polymer fixed on a fibrous substrate with good stability can be obtained. The present invention has been achieved by finding that it can be easily and inexpensively obtained.

すなわち、本発明による吸水性複合材料の製造法は、下
記の工程の結合からなること、を特徴とするものであ
る。
That is, the method for producing a water absorbent composite material according to the present invention is characterized by comprising the following steps of bonding.

(A)カルボキシル基の20%以上がアルカリ金属塩また
はアンモニウム塩に中和されているアクリル酸を主成分
とする重合性モノマーの水溶液を、成形した繊維質基体
に施す工程。
(A) A step of applying to a molded fibrous substrate an aqueous solution of a polymerizable monomer containing acrylic acid as a main component in which 20% or more of carboxyl groups are neutralized with an alkali metal salt or an ammonium salt.

(B)この繊維質基体に施された重合性単量体を重合さ
せて、該重合性単量体由来の重合体と繊維質基体との複
合体を形成させる工程。
(B) A step of polymerizing the polymerizable monomer applied to the fibrous substrate to form a composite of the polymer derived from the polymerizable monomer and the fibrous substrate.

(C)上記複合体に、カルボキシル基および(または)
カルボキシレート基と反応しうる2個以上の官能基を有
する架橋剤化合物を、該複合体中の重合性単量体由来の
重合体1重量部につき0.01〜10重量部に相当する量の水
が存在する状態において添加して反応させる工程。
(C) The above complex has a carboxyl group and / or
A crosslinking agent compound having two or more functional groups capable of reacting with the carboxylate group is added in an amount of 0.01 to 10 parts by weight of water per 1 part by weight of the polymer derived from the polymerizable monomer in the composite. A step of adding and reacting in the existing state.

発明の効果 本発明の吸水性複合材料の製造法において、成形した繊
維質基体に施されたアクリル酸系モノマーは、そのほと
んどが重合して高吸水性ポリマーとなるために吸水性能
が大きくなること、さらに、該吸水性ポリマーは架橋処
理されることにより、吸水速度が特段に大きく、高吸水
性ポリマーが繊維質基体に安定性良く固定されること、
等の点において著しい特徴を有するものである。そして
この為に前記先行発明等よりも格段に優れた吸水性複合
材料が容易にしかも安価に得られる。
EFFECTS OF THE INVENTION In the method for producing a water-absorbing composite material of the present invention, most of acrylic acid-based monomers applied to a molded fibrous substrate are polymerized into a super-water-absorbing polymer, so that the water-absorbing performance is increased. Further, the water-absorbent polymer is crosslinked to have a particularly high water-absorption rate, and the highly water-absorbent polymer is stably fixed to the fibrous substrate,
It has remarkable features in terms of the above. Therefore, a water-absorbent composite material, which is far superior to the above-mentioned prior inventions, can be obtained easily and at low cost.

本発明での工程(C)の架橋処理は工程(B)により得
られる複合体中のアクリル酸系重合体のカルボキシル基
および(または)カルボキシレート基を架橋点とするも
のであるところ、本発明複合体の吸水性はカルボキシル
基および(または)カルボキシレート基の存在に少なく
とも部分的に負っていると解されるから、工程(C)に
よってこのような親水性の基を変性したことによって吸
水速度が向上したということは思いがけなかったことと
いうべできある。
The crosslinking treatment in the step (C) in the present invention uses the carboxyl group and / or the carboxylate group of the acrylic acid-based polymer in the composite obtained in the step (B) as crosslinking points. Since it is understood that the water absorption of the complex is at least partly due to the presence of the carboxyl group and / or the carboxylate group, the water absorption rate can be improved by modifying the hydrophilic group in step (C). It can be said that the improvement was unexpected.

〔発明の具体的説明〕[Specific Description of the Invention]

工程(A)および(B)モノマー 本発明に用いられるモノマーは、アクリル酸を主成分と
するが、その20%以上が、好ましくは50%以上が、アル
カリ金属塩又はアンモニウム塩に中和されているもので
ある。その部分中和度が20%未満であると生成ポリマー
の吸水性能が著しく低下するので好ましくない。
Step (A) and (B) Monomer The monomer used in the present invention contains acrylic acid as a main component, but 20% or more, preferably 50% or more thereof is neutralized with an alkali metal salt or an ammonium salt. There is something. If the degree of partial neutralization is less than 20%, the water absorption performance of the produced polymer is significantly deteriorated, which is not preferable.

また本発明では、上記アクリル酸及びアクリル酸塩以外
にこれらと共重合可能な単量体、例えば2−アクリルア
ミド−2−メチルプロパンスルホン酸、2−アクリロイ
ルエタンスルホン酸、2−アクリロイルプロパンスルホ
ン酸、メタクリル酸およびそれらのアルカリ金属塩又は
アンモニウム塩、(メタ)アクリルアミド、N,N−ジメ
チル(メタ)アクリルアミド、2−ヒドロキシエチル
(メタ)アクリルアミド、2−ヒドロキシエチル(メ
タ)アクリレート、2−ヒドロキシプロピル(メタ)ア
クリレート、ポリエチレングリコールモノ(メタ)アク
リレート、N,N′−メチレンビス(メタ)アクリルアミ
ドおよびポリエチレングリコールジ(メタ)アクリレー
トからなる群から選ばれる1種又は2種以上を添加する
ことにより、吸水性能がより高いものが得られる場合が
ある。ここで、「(メタ)アクリル」は、アクリルおよ
びメタクリルを意味するものである。アクリル酸および
アクリル酸塩と共重合可能な他の単量体、例えば、イタ
コン酸、マレイン酸、フマール酸、ビニルスルホン酸及
びそれらのアルカリ金属塩又はアンモニウム塩等の水溶
性モノマーが、また本発明の「重合性モノマーの水溶
液」が形成される限り、アクリル酸メチル、アクリル酸
エチル等のアクリル酸アルキルエステル類等の低水溶性
モノマーが、併用可能である。
Further, in the present invention, in addition to the acrylic acid and the acrylic acid salt, a monomer copolymerizable with them, for example, 2-acrylamido-2-methylpropanesulfonic acid, 2-acryloylethanesulfonic acid, 2-acryloylpropanesulfonic acid, Methacrylic acid and its alkali metal salts or ammonium salts, (meth) acrylamide, N, N-dimethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylamide, 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl ( Water absorption performance by adding one or more selected from the group consisting of (meth) acrylate, polyethylene glycol mono (meth) acrylate, N, N′-methylenebis (meth) acrylamide and polyethylene glycol di (meth) acrylate. Gayo There are cases where high is obtained. Here, "(meth) acrylic" means acrylic and methacrylic. Other monomers copolymerizable with acrylic acid and acrylates, for example water-soluble monomers such as itaconic acid, maleic acid, fumaric acid, vinylsulphonic acid and their alkali metal or ammonium salts, are also included in the invention. As long as the “aqueous solution of polymerizable monomer” is formed, a low water-soluble monomer such as alkyl acrylates such as methyl acrylate and ethyl acrylate can be used in combination.

本発明での「重合性モノマー」はアクリル酸(そのうち
の20%以上は塩の形態である)を主成分とするものであ
るから、上記の共重合性単量体の添加量は、一般的には
50モル%未満であり、好ましくは20%以下が採用され
る。
Since the "polymerizable monomer" in the present invention is mainly composed of acrylic acid (of which 20% or more is in the form of a salt), the amount of the above-mentioned copolymerizable monomer added is generally In
It is less than 50 mol%, preferably 20% or less.

なお、アクリル酸をはじめとする上記のような酸モノマ
ーの中和にはアルカリ金属の水酸化物や重炭酸塩等又は
水酸化アンモニウム等が使用可能であるが、好ましいの
はアルカリ金属酸化物であり、その具体例としては水酸
化ナトリウム、水酸化カリウム及び水酸化リチウムが挙
げられる。工業的入手の容易さ、価格及び安全性等の点
から、水酸化ナトリウムあるいは水酸化カリウムが好ま
しい。
It should be noted that alkali metal hydroxides, bicarbonates, ammonium hydroxides, etc. can be used for neutralizing the above-mentioned acid monomers including acrylic acid, but alkali metal oxides are preferable. There are sodium hydroxide, potassium hydroxide and lithium hydroxide as specific examples. Sodium hydroxide or potassium hydroxide is preferred from the viewpoints of industrial availability, price, and safety.

本発明では、上記のようなアクリル酸(そのうちの20%
以上が塩となっている)を主体とする重合性モノマーを
水溶液の形で繊維質基体成形品に施す。この場合の水溶
液の濃度は、合目的的な任意の値でありうる。具体的に
は、たとえば、30重量%以上が適当である。
In the present invention, the acrylic acid as described above (of which 20%
The above is a salt) and a polymerizable monomer mainly containing the above is applied to the fibrous base molded article in the form of an aqueous solution. The concentration of the aqueous solution in this case can be any value that is purposeful. Specifically, for example, 30% by weight or more is suitable.

この水溶液は、本発明の目的に反しない限り、各種の物
質を含有していてもよい。そのような物質の一例は、水
溶液ラジカル重合開始剤である(詳細後記)。また、
「水溶液は、希望するならば水溶性有機溶媒が少量溶存
したものであってもい。
This aqueous solution may contain various substances as long as it is not against the object of the present invention. An example of such a substance is an aqueous solution radical polymerization initiator (detailed later). Also,
"The aqueous solution may be a solution of a small amount of a water-soluble organic solvent, if desired.

成形した繊維質基体 上記の重合体水溶液を施すべき成形した繊維質基体は、
具体的には、繊維をゆるく成形してなるもの、たとえ
ば、パット、カーディングもしくはエアレイイングした
ウエブ、ティッシュペーパー、木綿ガーゼの様な織布、
メリヤス地、又は不織布である。ここで、「成形した」
繊維質基体とは、その繊維質基体を用品の中に組み込む
ために、切断、接合、造形等が必要になることはある
が、ウエブ形成作業はさらに施す必要がないものを意味
する。
Molded fibrous substrate The molded fibrous substrate to which the above aqueous polymer solution is to be applied is
Specifically, a loosely formed fiber, for example, a pad, a carded or air-laid web, a tissue paper, a woven cloth such as cotton gauze,
It is a knitted fabric or a non-woven fabric. Where "molded"
The fibrous base material means a material which may require cutting, joining, shaping, or the like for incorporating the fibrous base material into a product, but does not require further web forming work.

木材パルプ、レーヨン、木綿その他のセルロース系繊維
および(または)ポリエステル系繊維の様な吸収性繊維
を主成分として繊維質基体に使用することが一般的に好
ましい。しかし他の種類の繊維、例えば、ポリエチレン
系、ポリプロピレン系、ポリスチレン系、ポリアミド
系、ポリビニールアルコール系、ポリ塩化ビニール系、
ポリ塩化ビニリデン系、ポリアクリロニトリル系、ポリ
尿素系、ポリウレタン系、ポリフルオロエチレン系、ポ
リシアン化ビニリデン系等のような繊維を成形した繊維
質基体に含ませてもよい。
It is generally preferred to use absorbent fibers such as wood pulp, rayon, cotton or other cellulosic fibers and / or polyester fibers as the major component in the fibrous substrate. However, other types of fibers such as polyethylene, polypropylene, polystyrene, polyamide, polyvinyl alcohol, polyvinyl chloride,
Fibers such as polyvinylidene chloride-based, polyacrylonitrile-based, polyurea-based, polyurethane-based, polyfluoroethylene-based, and polyvinylidene cyanide-based fibers may be contained in a molded fibrous substrate.

モノマー水溶液の施用およびモノマーの重合(一次重
合) 本発明では、前記のモノマー水溶液を上記の成形した繊
維基質に施し、そして、繊維基質上でモノマーを重合さ
せる(一次重合)。
Application of Aqueous Monomer Solution and Polymerization of Monomer (Primary Polymerization) In the present invention, the above-mentioned aqueous monomer solution is applied to the molded fiber substrate, and the monomer is polymerized on the fiber substrate (primary polymerization).

モノマー水溶液を成形繊維質基体に施すには、モノマー
が繊維質基体上に均一に分散保持され、そして重合しう
る限り、合目的的な任意の手段ないし態様によることが
できる。そのための典型的な手段の一つは、モノマー水
溶液を繊維質基体に含浸させるかあるいはモノマー水溶
液を繊維質基体に噴霧することである。
The aqueous monomer solution can be applied to the molded fibrous substrate by any purposeful means or modes as long as the monomer can be uniformly dispersed and held on the fibrous substrate and polymerized. One of the typical means for this is to impregnate the fibrous substrate with the aqueous monomer solution or to spray the aqueous monomer solution onto the fibrous substrate.

モノマー水溶液を繊維質基体に施す好ましい態様は、モ
ノマー水溶液を成形繊維質基体の繊維に沿って連続した
線条模様となるように施すか、あるいは繊維上に小さな
周期的な点状に施すことである。前者の態様では、モノ
マー水溶液を成形繊維質基質に含浸させあるいは多量に
噴霧して、繊維に付着ないし含浸させてから、繊維間の
モノマー水溶液を吸引除去する方法あるいはロールコー
ターにより塗布する方法等によって成形繊維基質に施
す。後者の態様ではモノマー水溶液が成形繊維質基体に
噴霧することによって施すが、その場合の粒子径は30〜
500μm、好ましくは30〜200μm程度となるように噴霧
条件を設定することが好ましい。
A preferred embodiment of applying the monomer aqueous solution to the fibrous substrate is to apply the monomer aqueous solution so as to form a continuous linear pattern along the fibers of the molded fibrous substrate, or to apply it in small periodic dots on the fibers. is there. In the former embodiment, a method of impregnating or spraying a large amount of an aqueous monomer solution onto a molded fibrous substrate to adhere or impregnate the fibers, and then removing the aqueous monomer solution between the fibers by suction or applying by a roll coater is used. Apply to molded fiber substrate. In the latter embodiment, the aqueous monomer solution is applied by spraying on the molded fibrous substrate, in which case the particle size is 30 to
It is preferable to set the spraying conditions so as to be about 500 μm, preferably about 30 to 200 μm.

また、このように繊維質基体上に均一分散したモノマー
を重合させる段階も、合目的的な任意のものでありう
る。そのような方法の典型的なものは、水溶性ラジカル
重合開始剤の作用によるもの、具体的には、モノマー水
溶液中にラジカル重合開始剤を添加しておいて繊維質基
体上でそれを分解させるか、あるいはラジカル重合開始
剤をモノマーとは別の溶液としてモノマー溶液施用後の
繊維質基体に噴霧等によって均一に施して、繊維質基体
上で分解させるか、あるいはラジカル重合開始剤をモノ
マーとは別の溶液として繊維質基体に施しておいて、そ
こへモノマー水溶液を噴霧、塗布等によって均一に施す
ことである。重合開始の他の手段は、高エネルギー放射
線の照射である。
Also, the step of polymerizing the monomer uniformly dispersed on the fibrous substrate in this manner may be a purposeful one. A typical example of such a method is by the action of a water-soluble radical polymerization initiator, specifically, the radical polymerization initiator is added to an aqueous monomer solution and decomposed on the fibrous substrate. Alternatively, the radical polymerization initiator is uniformly applied to the fibrous substrate after application of the monomer solution as a solution separate from the monomer by spraying or the like to decompose on the fibrous substrate, or the radical polymerization initiator is different from the monomer. The solution is applied to the fibrous substrate as another solution, and the aqueous monomer solution is uniformly applied thereto by spraying or coating. Another means of initiating polymerization is irradiation with high energy radiation.

本発明で使用する水溶性ラジカル重合開始剤は、高分子
化学の分野において周知のものである。具体的には、無
機または有機過酸化物たとえば過硫酸塩(アンモニウム
塩、アルカリ金属塩(特にカリウム塩)その他)、過酸
化水素、ジ第三ブチルペルオキシド、アセチルペルオキ
シド、その他、がある。これらの過酸化物の外に、所定
の水溶性が得られるならば、アゾ化合物その他のラジカ
ル重合開始剤、たとえば2,2′−アゾビス(2−アミジ
ノプロパン)二塩酸塩、も使用可能である。
The water-soluble radical polymerization initiator used in the present invention is well known in the field of polymer chemistry. Specific examples include inorganic or organic peroxides such as persulfates (ammonium salts, alkali metal salts (particularly potassium salts) and the like), hydrogen peroxide, ditertiary butyl peroxide, acetyl peroxide, and the like. In addition to these peroxides, azo compounds and other radical polymerization initiators such as 2,2'-azobis (2-amidinopropane) dihydrochloride can be used as long as a predetermined water solubility is obtained. .

重合はこれらのラジカル重合開始剤の分解によって開始
される訳であるが、分解のための慣用の手段である加熱
(モノマーと接触したときの温度が既に分解温度である
場合が多く、特に加熱をしなくても重合開始剤をモノマ
ーに添加するだけで重合が開始される場合をこの明細書
では加熱による分解の範疇に入れるものとする)の外
に、化学物質によって重合開始剤の分解を促進すること
もまた周知の手段である。重合開始剤が過酸化物である
ときのその分解促進物質は還元性化合物(本発明では水
溶性のもの)たとえば過硫酸塩に対しては酸性亜硫酸
塩、アスコルビン酸、アミン等であって、過酸化物と還
元性化合物との組合せからなる重合開始剤は「レドック
ス開始剤」として高分子化学の分野で周知のものであ
る。従って、本発明で「重合開始剤」という用語は、こ
のような分解促進物質との組合せ、特にレドックス開始
剤、を包含するものである。
Polymerization is initiated by the decomposition of these radical polymerization initiators, but heating which is a conventional means for decomposition (the temperature at the time of contact with the monomer is often already the decomposition temperature, especially heating is (In this specification, the case where the polymerization is started only by adding the polymerization initiator to the monomer is not included in the scope of the decomposition by heating in this specification), and the decomposition of the polymerization initiator is promoted by chemical substances. Doing is also a well-known means. When the polymerization initiator is a peroxide, the decomposition accelerating substance is a reducing compound (a water-soluble compound in the present invention) such as an acid sulfite, ascorbic acid, amine or the like for a persulfate. A polymerization initiator composed of a combination of an oxide and a reducing compound is well known in the field of polymer chemistry as a "redox initiator". Therefore, in the present invention, the term "polymerization initiator" includes a combination with such a decomposition promoting substance, particularly a redox initiator.

高エネルギー放射線としては、電磁放射線や微粒子イオ
ン化放射線等がある。
High energy radiation includes electromagnetic radiation and fine particle ionizing radiation.

このような重合開始手段、特に水溶性ラジカル重合開始
剤によるアクリル酸(そのうちの20%以上は塩の形であ
る)主体モノマーの重合によって生成するのは、このモ
ノマーにN,N′−メチレンビス(メタ)アクリルアミド
のようなジエチレン性モノマーを使用しない限り非架橋
の水溶性ポリマーである筈であるが、実際上はアクリル
酸(塩)ないしそのポリマー相互の間または/および繊
維質基体との間で架橋反応が生じることが認められてい
る。従って、この工程で生成するポリアクリル酸(塩)
は、水溶性ポリマーというよりも高吸水性ポリマーとい
うことになる。
Such polymerization initiation means, in particular, the polymerization of acrylic acid (of which 20% or more is in the form of a salt) -based monomer with a water-soluble radical polymerization initiator produces N, N'-methylenebis ( It should be a non-crosslinked water-soluble polymer unless a diethylenic monomer such as (meth) acrylamide is used, but in practice it is between acrylic acid (salt) or its polymers or / and between fibrous substrates. It is recognized that a crosslinking reaction occurs. Therefore, polyacrylic acid (salt) produced in this process
Is a superabsorbent polymer rather than a water-soluble polymer.

なお、水溶性ラジカル重合開始剤による重合は、実質的
に水溶液重合であるべきである。従って、工程(B)は
過度に乾燥した状態を避けて実施すべきである。
The polymerization with the water-soluble radical polymerization initiator should be substantially aqueous solution polymerization. Therefore, step (B) should be carried out avoiding excessively dry conditions.

工程(A)によって繊維質基体に施されたモノマーの賦
存量は、繊維質基体100重量部につき1〜10000重量部、
好ましくは10〜1000重量部、である。このようにして施
されたモノマーは、その50%以上、好ましくは80%以
上、が工程(B)で重合すべきである。工程(B)で80
〜95%程度の重合率が得られることがふつうである。
The amount of the monomer applied to the fibrous substrate in the step (A) is 1 to 10,000 parts by weight per 100 parts by weight of the fibrous substrate,
It is preferably 10 to 1000 parts by weight. At least 50%, preferably at least 80% of the monomers applied in this way should be polymerized in step (B). 80 in process (B)
It is usual to obtain a polymerization rate of about 95%.

上記したところに基いて、工程(A)および(B)の具
体例のいくつかを示せば、下記の通りである。
Based on the above, some of the specific examples of the steps (A) and (B) are shown below.

(1)25%以上のモノマー濃度を有するアクリル酸系モ
ノマー水溶液と水溶性ラジカル重合開始剤とを予め均一
混合後、繊維質基体中の高吸水性ポリマー粒径が30〜50
0μmなる様に該混合液を霧状にして成形した繊維質基
体に施し、重合開始剤がレドックス系でない場合は加熱
して重合させる方法(特願昭60-193403号参照)、
(2)少量の架橋剤を含むアクリル酸系モノマーの水溶
液と水溶性ラジカル重合開始剤とを予め均一混合後、繊
維質基体中の高吸水性ポリマー粒子径が30〜500μmと
なる様に該混合液を霧状にして成形した繊維質基体に施
し、重合開始剤がレドックス系でない場合は加熱して重
合させる方法(特願昭60-202908号参照)、(3)少量
の架橋剤を含むアクリル酸系モノマーの水溶液と酸化性
のラジカル重合開始剤とを混合液、繊維質基体に施し、
その後にアミン類又は還元剤を施してレドックス系を形
成させて重合を開始させる方法(特願昭60-238421号参
照)、(4)少量の架橋剤を含むアクリル酸系モノマー
の水溶液と、アミン類又は還元剤とを混合後、繊維質基
体に施し、その後に酸化性ラジカル重合開始剤を施して
レドックス系を形成させて重合を開始させる方法(特願
昭60-238420号参照)、(5)アクリル酸系モノマー水
溶液を予め繊維質基体に含浸させた後、水溶性ラジカル
重合開始剤を霧状にして添加し、重合開始剤がレドック
ス系でない場合は加熱して重合を開始させる方法(特開
昭60-149609号公報)等々。
(1) An acrylic acid-based monomer aqueous solution having a monomer concentration of 25% or more and a water-soluble radical polymerization initiator are uniformly mixed in advance, and the superabsorbent polymer particle size in the fibrous substrate is 30 to 50.
A method in which the mixed solution is atomized to a particle size of 0 μm and applied to a molded fibrous substrate, and when the polymerization initiator is not a redox system, heating is performed to perform polymerization (see Japanese Patent Application No. 60-193403).
(2) An aqueous solution of an acrylic acid-based monomer containing a small amount of a cross-linking agent and a water-soluble radical polymerization initiator are uniformly mixed in advance, and then mixed so that the superabsorbent polymer particle size in the fibrous substrate is 30 to 500 μm. A method in which the liquid is atomized and applied to a molded fibrous substrate, and when the polymerization initiator is not a redox type, the polymerization is carried out by heating (see Japanese Patent Application No. 60-202908), (3) Acrylic containing a small amount of a crosslinking agent An aqueous solution of an acid-based monomer and an oxidizing radical polymerization initiator are mixed on a fibrous substrate,
Thereafter, a method of applying a amine or a reducing agent to form a redox system to initiate polymerization (see Japanese Patent Application No. 60-238421), (4) an aqueous solution of an acrylic acid-based monomer containing a small amount of a crosslinking agent, and an amine Or a reducing agent is mixed and then applied to a fibrous substrate, and then an oxidizing radical polymerization initiator is applied to form a redox system to initiate polymerization (see Japanese Patent Application No. 60-238420), (5) ) A method of impregnating a fibrous substrate with an acrylic acid-based monomer aqueous solution in advance and then adding a water-soluble radical polymerization initiator in the form of a mist, and heating the polymerization initiator by heating when the polymerization initiator is not a redox system (special (Kaisho 60-149609 publication) and so on.

工程(C) 架橋処理 架橋処理は、上記のようにして得られる複合体中の該重
合体由来のカルボキシル基および(または)カルボキシ
レート基をそれと反応する官能基を少なくとも2個持つ
架橋剤化合物と反応させることからなる。
Step (C) Crosslinking Treatment The crosslinking treatment is carried out with a crosslinking agent compound having at least two functional groups which react with the carboxyl group and / or carboxylate group derived from the polymer in the composite obtained as described above. Consists of reacting.

本発明で使用する架橋剤化合物の上記のような官能基と
しては、エトキシル基、アルデヒド基、アルキル性ヒド
ロキシル基、第一〜第二アミン基、その他、がある。
The above-mentioned functional groups of the crosslinking agent compound used in the present invention include an ethoxy group, an aldehyde group, an alkyl hydroxyl group, a primary to secondary amine group, and others.

このような官能基を少なくとも2個有する化合物として
は、従ってエチレングリコールジグリシジルエーテル、
ポリエチレングリコールジグリシジルエーテル等のポリ
グリジルエーテル類、エピクロルヒドリン等のハロエポ
キシ化合物、グルタルアルデヒド、グルオキザール等の
ポリアルデヒド類、エチレングリコール、グリセリン等
のポリオール類、エチレンジアミン等のポリアミン類な
どが挙げられる。これらのうちでも、ポリグリシジルエ
ーテル類が好ましい。
A compound having at least two such functional groups is, therefore, ethylene glycol diglycidyl ether,
Examples thereof include polyglycidyl ethers such as polyethylene glycol diglycidyl ether, haloepoxy compounds such as epichlorohydrin, polyaldehydes such as glutaraldehyde and gluoxal, polyols such as ethylene glycol and glycerin, and polyamines such as ethylenediamine. Among these, polyglycidyl ethers are preferable.

架橋反応は、工程(B)からの複合体に架橋剤化合物を
均一に添加して反応させることによって進行させること
ができる。その場合に留意すべきことは、この複合体の
水分である。すなわち、この複合体が過度に水を含んで
いると、また過度に乾燥していると、効率よく架橋化が
起らず、本発明が目的とする吸水速度の複合効果は極め
て小さいものとなってしまう。複合体の含水量は、複合
体中の重合性単量体由来の重合体1重量部につき0.01〜
10重量部、特に0.1〜1重量部、である。
The cross-linking reaction can be proceeded by uniformly adding the cross-linking agent compound to the complex from the step (B) and reacting it. In that case, it is the water content of this complex that should be noted. That is, if this complex contains excessive water, and if it is excessively dried, efficient cross-linking does not occur, and the combined effect of the water absorption rate aimed at by the present invention is extremely small. Will end up. The water content of the composite is from 0.01 to 1 part by weight of the polymer derived from the polymerizable monomer in the composite.
10 parts by weight, especially 0.1 to 1 part by weight.

架橋剤化合物の添加量は、重合性単量体由来の重合体の
0.01〜10%、好ましくは0.1〜5%(重量)、程度であ
る。
The amount of the crosslinking agent compound added is the amount of the polymer derived from the polymerizable monomer.
It is about 0.01 to 10%, preferably 0.1 to 5% (by weight).

架橋反応条件は、使用する架橋剤化合物の種類によって
変化するが、一般的には50〜200℃、好ましくは100〜15
0℃程度の温度、および数秒〜5時間、好ましくは数秒
〜1時間、程度のの時間である。
The crosslinking reaction conditions vary depending on the kind of the crosslinking agent compound used, but generally 50 to 200 ° C., preferably 100 to 15
The temperature is about 0 ° C. and the time is about several seconds to 5 hours, preferably several seconds to 1 hour.

架橋剤化合物の使用量は上記のように少ないから、この
ような少量の架橋剤化合物を工程(B)からの複合体に
均一に添加するには溶液の形で塗布または噴霧あるいは
含浸させるのがよい。
Since the amount of the crosslinking agent compound used is small as described above, in order to uniformly add such a small amount of the crosslinking agent compound to the complex from the step (B), it is necessary to apply, spray or impregnate in the form of a solution. Good.

反応方法ないし装置は、合目的的な任意のものでありう
る。具体的には、たとえば、内部を所定温度に設定した
ボックス形反応器によって回分式に加熱する方法、スチ
ーム等によって所定の表面温度に設定されたローラーに
対象複合体を連続的に接触させる連続加熱方法、その他
がある。
The reaction method or device can be any purposeful. Specifically, for example, a method of heating the inside in a batch manner by a box-type reactor set to a predetermined temperature, continuous heating in which a target complex is continuously brought into contact with a roller set to a predetermined surface temperature by steam or the like. There are other ways.

加熱時の雰囲気としては、真空下または窒素、アルゴ
ン、ヘリウム等の無機ガス存在下、または空気中のいず
れも使用できる。好ましい雰囲気は空気である。
The atmosphere during heating may be either under vacuum or in the presence of an inorganic gas such as nitrogen, argon or helium, or in air. The preferred atmosphere is air.

実験例 実施例1 100ccのコニカルフラスコに、水酸化ナトリウム(純度9
6重量%)13.1gを採り、これに氷冷下アクリル酸30gを
徐々に加え中和した。中和度は約75%、水溶液中のモノ
マー濃度として約45重量%となった。
Experimental Example Example 1 Sodium hydroxide (purity 9
(6% by weight) 13.1 g was taken, and 30 g of acrylic acid was gradually added thereto under ice cooling to neutralize. The degree of neutralization was about 75%, and the monomer concentration in the aqueous solution was about 45% by weight.

これにラジカル重合開始剤として過硫酸カリウムを0.05
g採って、上記モノマー水溶液中に溶解させ、N2にて脱
気した。
0.05% of potassium persulfate as a radical polymerization initiator
g was taken, dissolved in the above monomer aqueous solution, and degassed with N 2 .

別にポリエステル不織布を0.583g採って、これに上記モ
ノマー水溶液をロールコーターによって不織布全面に塗
布して繊維に沿って線条模様に施した。含浸されたモノ
マー量は、不織布に対して6.8重量倍であった。これ
を、あらかじめN2で脱気して90℃にした恒温反応槽内に
入れた。重合は直ちに起って、部分中和ポリアクリル酸
ソーダの自己架橋物からなる高吸水性ポリマーがポリエ
ステル不織布にその繊維に沿って線条模様に安定性良く
固定された複合体が得られた。
Separately, 0.583 g of a polyester non-woven fabric was taken, and the above-mentioned aqueous monomer solution was applied to the whole surface of the non-woven fabric by a roll coater to form a linear pattern along the fibers. The amount of the impregnated monomer was 6.8 times the weight of the nonwoven fabric. This was placed in a constant temperature reaction vessel that had been degassed with N 2 in advance to 90 ° C. Polymerization occurred immediately, and a superabsorbent polymer consisting of a self-crosslinked product of partially neutralized sodium polyacrylate was fixed to the polyester nonwoven fabric along the fibers in a linear pattern with good stability.

次いで、この複合体の水分量を約25重量%(高吸水性ポ
リマー重量基準。以下、同様)とし、これにエチレング
リコールジグリシジルエーテル0.017gを溶液として噴霧
してから、120℃に設定された恒温層の中に15分間置い
て、吸水性複合材料を得た。
Next, the water content of this complex was adjusted to about 25% by weight (based on the weight of the superabsorbent polymer; hereinafter the same), 0.017 g of ethylene glycol diglycidyl ether was sprayed as a solution, and then set to 120 ° C. It was placed in a constant temperature layer for 15 minutes to obtain a water absorbent composite material.

得られた吸水性複合材料の諸特性は下記の通りであった
(以下の製造例において同じ)。
The properties of the obtained water-absorbent composite material were as follows (the same applies to the following production examples).

実施例2 100ccコニカルフラスコに水酸化ナトリウム(純度95重
量%)13.1gを採って、氷冷下に純水39.0gで溶した。こ
れにアクリル酸30gを氷冷下に注入して中和させた。ア
クリル酸中和度約75%、水溶液中のモノマー濃度として
約45重量%となった。これに架橋性単量体としてN,N′
−メチレンビスアクリルアミドを0.005g、ラジカル重合
開始剤として2,2′−アゾビス(2−アミジノプロパ
ン)二塩酸塩0.1g採って、前記モノマー水溶液中に溶解
し、脱気を行った。
Example 2 13.1 g of sodium hydroxide (purity: 95% by weight) was placed in a 100 cc conical flask and dissolved in 39.0 g of pure water under ice cooling. To this, 30 g of acrylic acid was poured under ice cooling for neutralization. The degree of neutralization of acrylic acid was about 75%, and the monomer concentration in the aqueous solution was about 45% by weight. N, N ′ as a crosslinkable monomer
0.005 g of methylenebisacrylamide and 0.1 g of 2,2'-azobis (2-amidinopropane) dihydrochloride as a radical polymerization initiator were taken, dissolved in the aqueous monomer solution and deaerated.

別にポリエステル不織布を0.655g採り、これに上記原料
を不織布全面にロールコーターで塗布して繊維に沿って
線条模様に施した。含浸されたモノマー量は、不織布に
対して7.5重量倍であった。これを、予めN2で脱気させ
て90℃にした恒温反応槽内に入れた。重合は直ちに起っ
て、部分中和ポリアクリル酸ナトリウムのN,N′−メチ
レンビスアクリルアミド架橋物からなる高吸水性ポリマ
ーがポリエステル不織布にその繊維に沿って線条模様に
安定性良く固定された複合体が得られた。
Separately, 0.655 g of a polyester non-woven fabric was taken, and the above raw materials were applied to the entire surface of the non-woven fabric by a roll coater to form a linear pattern along the fiber. The amount of the impregnated monomer was 7.5 times the weight of the nonwoven fabric. This was placed in a constant temperature reaction tank that had been degassed with N 2 in advance and kept at 90 ° C. Polymerization occurred immediately, and a superabsorbent polymer consisting of N, N'-methylenebisacrylamide cross-linked product of partially neutralized sodium polyacrylate was stably fixed to the polyester non-woven fabric along the fiber in a linear pattern. A complex was obtained.

次いで、この複合体の水分量を約28重量%とし、エチレ
ングリコールグリシジルエーテル0.025gを添加して120
℃に設定された恒温層中に15分間置いて、吸水性複合材
料を得た。
Next, the water content of this complex was adjusted to about 28% by weight, and 0.025 g of ethylene glycol glycidyl ether was added to the mixture to give 120%.
It was placed in a constant temperature layer set at 0 ° C for 15 minutes to obtain a water absorbent composite material.

実施例3 100ccコニカルフラスコにアクリル酸30gを採り、これに
純水9.3gを加えて混合した。これに、氷冷下に水酸化カ
リウム(85重量%)20.6を徐々に加えて中和し、70℃に
保つ。中和度は約75%、水溶液中のモノマー濃度は約74
重量%となった。
Example 3 30 g of acrylic acid was placed in a 100 cc conical flask, and 9.3 g of pure water was added thereto and mixed. To this, potassium hydroxide (85% by weight) 20.6 was gradually added under ice cooling to neutralize, and the temperature was maintained at 70 ° C. The degree of neutralization is about 75%, and the monomer concentration in the aqueous solution is about 74.
It became weight%.

別にラジカル重合開始剤として過硫酸カリウム0.2gを水
3.0gに溶解した。
Separately, 0.2 g of potassium persulfate was added to water as a radical polymerization initiator.
It dissolved in 3.0 g.

別にレーヨン不織布を0.5869g採り、これを恒温槽内に
て約70℃に保った。上記モノマー水溶液中にラジカル重
合開始剤水溶液を混合後、直ちにスプレーノズルより上
記不織布に噴霧した。重合は不織布内にて直ちに起っ
て、部分中和ポリアクリル酸カリウムの自己架橋物から
なる高吸水性ポリマーがポリエステル不織布に安定性良
く固定された複合体が得られた。塗布されたモノマー量
は、不織布に対して12重量倍であり、高吸水性ポリマー
の粒子径は100〜300μmであった。
Separately, 0.5869 g of rayon nonwoven fabric was sampled and kept at about 70 ° C. in a constant temperature bath. Immediately after the radical polymerization initiator aqueous solution was mixed with the monomer aqueous solution, the non-woven fabric was sprayed from a spray nozzle. Polymerization immediately took place in the nonwoven fabric, and a composite was obtained in which the superabsorbent polymer consisting of a self-crosslinked product of partially neutralized potassium polyacrylate was fixed to the polyester nonwoven fabric with good stability. The amount of the applied monomer was 12 times the weight of the nonwoven fabric, and the particle size of the superabsorbent polymer was 100 to 300 μm.

次に、この複合体の水分量を25重量%とし、これにエチ
レングリコールジグリシジルエーテル0.038gを添加し
て、120℃に設定された恒温槽中に15分間置いて、吸水
性複合材料を得た。
Next, the water content of this composite was adjusted to 25% by weight, 0.038 g of ethylene glycol diglycidyl ether was added thereto, and the mixture was placed in a thermostat set at 120 ° C for 15 minutes to obtain a water-absorbing composite material. It was

実施例4 100ccコニカルフラスコに25%アンモニア水26.0gを採
り、氷冷下に30gのアクリル酸を徐々に滴下して中和
し、70℃に昇温した。中和度は95%、水溶液中のモノマ
ー濃度は約55重量%となった。
Example 4 26.0 g of 25% ammonia water was placed in a 100 cc conical flask, and 30 g of acrylic acid was gradually added dropwise under ice cooling to neutralize and the temperature was raised to 70 ° C. The degree of neutralization was 95%, and the monomer concentration in the aqueous solution was about 55% by weight.

別にラジカル重合開始剤として過硫酸カリウム0.2gを水
3gに溶解した。
Separately, 0.2 g of potassium persulfate was added to water as a radical polymerization initiator.
Dissolved in 3 g.

別にポリエステル不織布を0.4695g採り、これを恒温槽
内にて約70℃に保った。上記モノマー水溶液中にラジカ
ル重合開始剤水溶液を混合後、直ちにスプレーノズルよ
り上記不織布に噴霧した。重合は不織布内にて直ちに起
って、部分中和ポリアクリル酸アンモニウムの自己架橋
物からなる高吸水性ポリマーがポリエステル不織布に安
定性良く固定された複合体が得られた。塗布されたモノ
マー量は、不織布に対して8重量倍であり、高吸水性モ
ノマーの粒子径は100〜250μmであった。
Separately, 0.4695 g of polyester non-woven fabric was sampled and kept at about 70 ° C. in a constant temperature bath. Immediately after the radical polymerization initiator aqueous solution was mixed with the monomer aqueous solution, the non-woven fabric was sprayed from a spray nozzle. Polymerization immediately occurred in the nonwoven fabric, and a composite having a highly water-absorbent polymer composed of a self-crosslinked product of partially neutralized ammonium polyacrylate stably fixed to the polyester nonwoven fabric was obtained. The amount of the applied monomer was 8 times the weight of the nonwoven fabric, and the particle diameter of the superabsorbent monomer was 100 to 250 μm.

次に、該複合体の水分量を15重量%とし、これにエチレ
ングリコールジグリシジルエーテル0.021gを添加して12
0℃に設定された恒温槽中に15分間置いて、吸水性複合
材料を得た。
Next, the water content of the complex was adjusted to 15% by weight, and 0.021 g of ethylene glycol diglycidyl ether was added to this to obtain 12
It was placed in a constant temperature bath set at 0 ° C. for 15 minutes to obtain a water absorbent composite material.

実施例5 100ccコニカルフラスコにアクリル酸30gを採って、これ
に純水16.9gを加えて混合した。これに氷冷下に水酸化
カリウム(85重量%)20.6gを徐々に加えて中和させ
た。中和度は約75%、水溶液中のモノマー濃度として約
65重量であった。
Example 5 30 g of acrylic acid was placed in a 100 cc conical flask, and 16.9 g of pure water was added thereto and mixed. Under ice cooling, 20.6 g of potassium hydroxide (85% by weight) was gradually added to neutralize. The degree of neutralization is about 75%, and the monomer concentration in the aqueous solution is about
It was 65 weight.

これに架橋剤としてN,N′−メチレンビスアクリルアミ
ドを0.1g採り、上記モノマー溶液に添加溶解させ、40℃
に加温した。これに更にラジカル重合開始剤として31%
過酸化水素水0.4gをとって溶解させた。
Take 0.1 g of N, N'-methylenebisacrylamide as a cross-linking agent and add to the above monomer solution to dissolve it.
Warmed to. In addition to this, 31% as a radical polymerization initiator
0.4 g of hydrogen peroxide water was taken and dissolved.

別にポリエステル不織布を0.6521g採り、これに上記原
料を不織布全面にロールコーターによって塗布含浸さ
せ、恒温反応槽内にて40℃に保った。含浸されたモノマ
ー量は、不織布に対して6.9重量倍であった。
Separately, 0.6521 g of a polyester non-woven fabric was taken, and the above raw materials were applied and impregnated on the entire surface of the non-woven fabric by a roll coater and kept at 40 ° C. in a constant temperature reaction tank. The amount of the impregnated monomer was 6.9 times the weight of the nonwoven fabric.

次に還元剤として5%L−アスコルビン酸水溶液をスプ
レーノズルより上記不織布全面に噴霧した。重合は直ち
に起り、部分中和ポリアクリル酸カリウムのN,N′−メ
チレンビスアクリルアミド架橋物からなる高吸水性ポリ
マーがポリエステル不織布に安定性良く固定された複合
体が得られた。
Next, a 5% L-ascorbic acid aqueous solution as a reducing agent was sprayed onto the entire surface of the non-woven fabric through a spray nozzle. Polymerization occurred immediately, and a superabsorbent polymer consisting of N, N'-methylenebisacrylamide crosslinked product of partially neutralized potassium polyacrylate was stably immobilized on the polyester nonwoven fabric to obtain a composite.

次に、この複合体の水分量を約30重量%とし、これにエ
チレングリコールジグリシジルエーテル0.023gを添加
し、120℃にした恒温反応槽内にて15分間処理して、吸
水性複合材料を得た。
Next, the water content of this composite was set to about 30% by weight, 0.023 g of ethylene glycol diglycidyl ether was added thereto, and the mixture was treated for 15 minutes in a constant temperature reaction tank kept at 120 ° C to give a water-absorbing composite material. Obtained.

実施例6 100ccフラスコにアクリル酸30gを採り、これに純水16.9
gを加えて混合した。これに氷冷下に水酸化カリウム(8
5重量%)20.6gを徐々に加えて中和させた。中和度は約
75%、水溶液中のモノマー濃度として約65重量%であっ
た。
Example 6 30 g of acrylic acid was placed in a 100 cc flask, and 16.9 of pure water was added to it.
g was added and mixed. Add potassium hydroxide (8
(5 wt%) 20.6 g was gradually added to neutralize. Neutralization degree is about
It was 75%, and the monomer concentration in the aqueous solution was about 65% by weight.

別にポリエステル不織布を0.6925g採り、これに上記原
料を不織布全面に塗布ロールコーターによって含浸させ
た。含浸されたモノマー量は、不織布に対して7.5重量
倍であった。
Separately, 0.6925 g of polyester non-woven fabric was taken, and the above raw materials were applied to the entire surface of the non-woven fabric and impregnated with a roll coater. The amount of the impregnated monomer was 7.5 times the weight of the nonwoven fabric.

次にこの部分中和アクリル酸カリウムモノマー水溶液を
含浸した不織布上に、ダイナミトロン加速器を装備した
電子線装置より、20メガラドの線量で電子線を照射し
た。重合は直ちに起り、部分中和ポリアクリル酸カリウ
ムの自己架橋体からなる高吸水性ポリマーがポリエステ
ル不織布にその繊維に沿って線状模様に安定性良く固定
された複合体が得られた。
Next, the non-woven fabric impregnated with the partially neutralized potassium acrylate monomer aqueous solution was irradiated with an electron beam at a dose of 20 megarads from an electron beam apparatus equipped with a dynamitron accelerator. Polymerization occurred immediately, and a superabsorbent polymer consisting of a self-crosslinked body of partially neutralized potassium polyacrylate was fixed to the polyester nonwoven fabric along the fibers in a linear pattern with good stability.

次に、この複合体の水分量を25重量%とし、これにエチ
レングリコールジグリシジルエーテル0.029gを添加し、
120℃にした恒温反応槽内で15分間処理して、吸水性複
合材料を得た。
Next, the water content of this composite was adjusted to 25% by weight, and 0.029 g of ethylene glycol diglycidyl ether was added thereto,
The mixture was treated for 15 minutes in a constant temperature reaction vessel kept at 120 ° C to obtain a water absorbent composite material.

実施例7 実施例1におけるエチレングリコールジグリシジルエー
テルの代りにプロピレングリコールジグリシジルエーテ
ル0.025gを使用した以外は実施例1と同処方、同操作に
て処理して、吸水性複合材料を得た。
Example 7 A water absorbent composite material was obtained by the same procedure and operation as in Example 1, except that 0.025 g of propylene glycol diglycidyl ether was used in place of the ethylene glycol diglycidyl ether in Example 1.

実施例8 実施例3におけるエチレングリコールジグリシジルエー
テルの代りにネオペンチルグリコールジグリシジルエー
テル0.045gを使用した以外は実施例3と同処方、同操作
にて処理して、吸水性複合材料を得た。
Example 8 A water absorbent composite material was obtained by the same procedure and operation as in Example 3, except that 0.045 g of neopentyl glycol diglycidyl ether was used in place of the ethylene glycol diglycidyl ether in Example 3. .

実施例9 実施例5におけるエチレングリコールジグリシジルエー
テルの代りにグリセロールポリグリシジルエーテル0.04
0gを使用した以外は実施例5と同処方、同操作にて処理
して、吸水性複合材料を得た。
Example 9 Instead of ethylene glycol diglycidyl ether in Example 5, glycerol polyglycidyl ether 0.04
A water-absorbent composite material was obtained by the same procedure and treatment as in Example 5, except that 0 g was used.

比較例1〜6 実施例1〜6において得られた複合体、即ちエチレング
リコールジグリシジルエーテルを添加いないで得られた
複合体、をそれぞれ比較例1〜6とした。
Comparative Examples 1 to 6 The composites obtained in Examples 1 to 6, that is, the composites obtained without adding ethylene glycol diglycidyl ether were designated as Comparative Examples 1 to 6, respectively.

以上の実施例で得られた吸水性複合材料及び比較例で得
られた複合体について、下記の生理塩水吸水能、及び未
重合モノマー濃度の各試験を行った。その結果は、第1
表に示すとおりであった。
With respect to the water-absorbent composite materials obtained in the above Examples and the composites obtained in Comparative Examples, the following tests of physiological saline water absorption capacity and unpolymerized monomer concentration were conducted. The result is the first
It was as shown in the table.

A.生理塩水吸水能 300mlのビーカーに複合体又は吸水性複合材料を約0.5g
及び濃度0.9重量%の食塩水約200gをそれぞれ秤量して
入れてから、約4時間放置して食塩水によってポリマー
を充分に膨潤させた。次いで、100メッシュ篩で水切り
をした後、その過食塩水量を秤量し、下記式にしたが
って生理塩水吸水能を算出する。
A. About 0.5g of composite or water-absorbent composite material in a beaker with a physiological saline absorption capacity of 300ml.
And about 200 g of a 0.9% strength by weight saline solution were weighed and put therein, respectively, and allowed to stand for about 4 hours to sufficiently swell the polymer with the saline solution. Then, after draining with a 100-mesh sieve, the amount of super saline solution is weighed, and the physiological salt water absorption capacity is calculated according to the following formula.

B.吸水速度 300mlのビーカーに濃度0.9重量%の食塩水約800gを秤量
に入れる。次に、複合体または吸水性複合材料を約0.5g
秤量して、この食塩水中に入れる。5分後、100メッシ
ュ篩で水切りしてから、その過食塩水量を秤量し、上
記の式に基いて生理食塩水吸収能を求めて、これを吸水
速度とする。
B. Weigh about 800 g of 0.9 wt% saline in a beaker with a water absorption rate of 300 ml. Next, about 0.5 g of composite or absorbent composite
Weigh and place in this saline solution. After 5 minutes, water was drained through a 100-mesh sieve, the amount of the super saline solution was weighed, the physiological saline absorption capacity was determined based on the above formula, and this was taken as the water absorption rate.

結果は、下表に示す通りであった。The results are shown in the table below.

本発明の製造法によって得られる吸水性複合材料は、上
記実施例及び比較例から明らかな様に前記先行発明等に
比べて吸水速度が格段に大きいものである。さらにその
形態がシート状である為に、従来使用されてきた粉末状
吸水性樹脂に比べて取扱いが容易で、安価である為に、
生理用ナプキン、紙おしめ、等各種の衛生材料の製造に
有利に使用できる。
The water-absorbent composite material obtained by the production method of the present invention has a remarkably high water-absorption rate as compared with the preceding inventions and the like, as is clear from the above Examples and Comparative Examples. Furthermore, since its form is a sheet, it is easier to handle and cheaper than powdered water-absorbent resins that have been used conventionally,
It can be advantageously used for manufacturing various sanitary materials such as sanitary napkins and diapers.

また、その優れた吸水性能および取扱い性を利用して、
本発明による製品は最近注目されてきた土壌改良剤、保
水剤等をはじめとする園芸用又は農業用の各種の材料の
製造にも使用することができる。
Also, by utilizing its excellent water absorption performance and handleability,
The product according to the present invention can also be used for the production of various materials for horticultural or agricultural purposes such as soil improvers and water retention agents, which have recently been receiving attention.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08F 2/00 MCT 265/02 MQM C08J 5/24 CEY 7310−4F D06M 13/11 15/263 D06M 13/18 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display location C08F 2/00 MCT 265/02 MQM C08J 5/24 CEY 7310-4F D06M 13/11 15/263 D06M 13/18

Claims (11)

【特許請求の範囲】[Claims] 【請求項1】下記の工程の結合からなることを特徴とす
る、吸水性複合材料の製造法。 (A)カルボキシル基の20%以上がアルカリ金属塩また
はアンモニウム塩に中和されているアクリル酸を主成分
とする重合性単量体の水溶液を、成形した繊維質基体に
施す工程。 (B)この繊維質基体に施された重合性単量体を重合さ
せて、該重合性単量体由来の重合体と繊維質基体との複
合体を形成させる工程。 (C)上記複合体に、カルボキシル基および(または)
カルボキシレート基と反応しうる2個以上の官能基を有
する架橋剤化合物を、該複合体中の重合性単量体由来の
重合体1重量部につき0.01〜10重量部に相当する量の水
が存在する状態において添加して反応させる工程。
1. A method for producing a water-absorbing composite material, which comprises the following steps. (A) A step of applying to a molded fibrous substrate an aqueous solution of a polymerizable monomer containing acrylic acid as a main component in which 20% or more of carboxyl groups are neutralized with an alkali metal salt or an ammonium salt. (B) A step of polymerizing the polymerizable monomer applied to the fibrous substrate to form a composite of the polymer derived from the polymerizable monomer and the fibrous substrate. (C) The above complex has a carboxyl group and / or
A crosslinking agent compound having two or more functional groups capable of reacting with the carboxylate group is added in an amount of 0.01 to 10 parts by weight of water per 1 part by weight of the polymer derived from the polymerizable monomer in the composite. A step of adding and reacting in the existing state.
【請求項2】重合性単量体が、カルボキシル基の20%以
上がアルカリ金属塩またはアンモニウム塩に中和されて
いるアクリル酸からなる、特許請求の範囲第1項記載の
方法。
2. The method according to claim 1, wherein the polymerizable monomer comprises acrylic acid having 20% or more of carboxyl groups neutralized with an alkali metal salt or an ammonium salt.
【請求項3】重合性単量体が、20モル%までの2−アク
リルアミド−2−メチルプロパンスルホン酸、2−アク
リロイルエタンスルホン酸、2−アクリロイルプロパン
スルホン酸、メタクリル酸、およびこれらのアルカリ金
属塩またはアンモニウム塩、アクリルアミド、メタクリ
ルアミド、N,N−ジメチルアクリルアミド、N,N−ジメチ
ルメタクリルアミド、2−ヒドロキシエチルアクリレー
ト、2−ヒドロキシエチルメタクリレート、2−ヒドロ
キシプロピルアクリレート、2−ヒドロキシプロピルメ
タクリレート、ポリエチレングリコールモノアクリレー
ト、ポリエチレングリコールモノメタクリレート、から
なる群から選ばれる少なくとも一種の単量体を含むもの
である、特許請求の範囲第1項記載の方法。
3. The polymerizable monomer comprises up to 20 mol% of 2-acrylamido-2-methylpropanesulfonic acid, 2-acryloylethanesulfonic acid, 2-acryloylpropanesulfonic acid, methacrylic acid, and alkali metals thereof. Salt or ammonium salt, acrylamide, methacrylamide, N, N-dimethylacrylamide, N, N-dimethylmethacrylamide, 2-hydroxyethyl acrylate, 2-hydroxyethyl methacrylate, 2-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, polyethylene The method according to claim 1, which comprises at least one monomer selected from the group consisting of glycol monoacrylate and polyethylene glycol monomethacrylate.
【請求項4】工程(A)での成形した繊維質基体が、セ
ルロース系繊維または(および)ポリエステル系繊維を
主成分とするものである、特許請求の範囲第1〜3項の
いずれか1項に記載の方法。
4. The method according to claim 1, wherein the fibrous substrate molded in the step (A) has a cellulosic fiber and / or a polyester fiber as a main component. The method described in the section.
【請求項5】工程(A)の繊維質基体が、繊維のゆるい
パッド、カーディングしたウエブ、エアレイイングした
ウエブ、紙、不織布、織布、またはメリヤス地である、
特許請求の範囲第1〜4項のいずれか1項に記載の方
法。
5. The fibrous substrate of step (A) is a loose pad of fibers, a carded web, an airlaid web, paper, a non-woven fabric, a woven fabric, or a knitted fabric.
The method according to any one of claims 1 to 4.
【請求項6】工程(A)での重合性単量体の水溶液を成
形した繊維質基体に施す段階が、該水溶液の該繊維質基
体への噴霧または該水溶液への該繊維質基体の含浸から
なる、特許請求の範囲第1〜5項のいずれか1項に記載
の方法。
6. The step of applying the aqueous solution of the polymerizable monomer in step (A) to the molded fibrous substrate comprises spraying the aqueous solution onto the fibrous substrate or impregnating the aqueous solution with the fibrous substrate. A method according to any one of claims 1 to 5, consisting of:
【請求項7】工程(A)で繊維質基体に施された重合性
モノマーの賦存量が、繊維質基体100重量部につき1〜1
0000重量部である、特許請求の範囲第1〜6項のいずれ
か1項に記載の方法。
7. The amount of the polymerizable monomer applied to the fibrous substrate in the step (A) is 1 to 1 per 100 parts by weight of the fibrous substrate.
The method according to any one of claims 1 to 6, which is 0000 parts by weight.
【請求項8】工程(B)での重合を、水溶性重合開始剤
の作用によって行なう、特許請求の範囲第1〜7項のい
ずれか1項に記載の方法。
8. The method according to claim 1, wherein the polymerization in step (B) is carried out by the action of a water-soluble polymerization initiator.
【請求項9】工程(B)での重合性単量体を水溶性ラジ
カル重合開始剤の作用によって重合させる段階が、重合
開始剤を重合単量体の水溶液に溶存させておいて分解さ
せるかあるいは重合開始剤を溶液状態で繊維質基体に噴
霧してから分解させることからなる、特許請求の範囲第
8項に記載の方法。
9. The step of polymerizing the polymerizable monomer in the step (B) by the action of the water-soluble radical polymerization initiator is to dissolve the polymerization initiator in an aqueous solution of the polymerization monomer to decompose it. Alternatively, the method according to claim 8, which comprises spraying a polymerization initiator in a solution state on a fibrous substrate and then decomposing the fibrous substrate.
【請求項10】工程(C)での架橋剤化合物が、カルボ
キシル基および(または)カルボキシレート基と反応す
る基としてグリシジル基を持つものである、特許請求の
範囲第1〜9項のいずれか1項に記載の方法。
10. The crosslinker compound in step (C) has a glycidyl group as a group that reacts with a carboxyl group and / or a carboxylate group, and any one of claims 1 to 9. The method according to item 1.
【請求項11】グリシジル基を持つ化合物がポリグリシ
ジルエーテルである、特許請求の範囲第10項記載の方
法。
11. The method according to claim 10, wherein the compound having a glycidyl group is polyglycidyl ether.
JP61201354A 1986-08-29 1986-08-29 Method for manufacturing water-absorbent composite material Expired - Lifetime JPH0780970B2 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
JP61201354A JPH0780970B2 (en) 1986-08-29 1986-08-29 Method for manufacturing water-absorbent composite material
US07/088,277 US4865886A (en) 1986-08-29 1987-08-24 Process for preparation of water absorptive composite material
TW076105007A TW255900B (en) 1986-08-29 1987-08-25
EP87112486A EP0262405B1 (en) 1986-08-29 1987-08-27 Process for the preparation of a water-absorptive fibrous material
ES198787112486T ES2027267T3 (en) 1986-08-29 1987-08-27 PROCEDURE FOR THE PREPARATION OF A FIBROUS WATER ABSORBENT MATERIAL.
DE8787112486T DE3774232D1 (en) 1986-08-29 1987-08-27 METHOD FOR PRODUCING WATER-ABSORBING, FIBROUS MATERIAL.
AU77661/87A AU600024B2 (en) 1986-08-29 1987-08-28 Process for preparation of water absorptive composite material
KR1019870009468A KR950013035B1 (en) 1986-08-29 1987-08-28 Process for the preparation of a water-absorptive fibrous material
CA000545646A CA1302806C (en) 1986-08-29 1987-08-28 Process for preparation of water absorptive composite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61201354A JPH0780970B2 (en) 1986-08-29 1986-08-29 Method for manufacturing water-absorbent composite material

Publications (2)

Publication Number Publication Date
JPS6357617A JPS6357617A (en) 1988-03-12
JPH0780970B2 true JPH0780970B2 (en) 1995-08-30

Family

ID=16439646

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61201354A Expired - Lifetime JPH0780970B2 (en) 1986-08-29 1986-08-29 Method for manufacturing water-absorbent composite material

Country Status (9)

Country Link
US (1) US4865886A (en)
EP (1) EP0262405B1 (en)
JP (1) JPH0780970B2 (en)
KR (1) KR950013035B1 (en)
AU (1) AU600024B2 (en)
CA (1) CA1302806C (en)
DE (1) DE3774232D1 (en)
ES (1) ES2027267T3 (en)
TW (1) TW255900B (en)

Families Citing this family (38)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0764896B2 (en) * 1987-04-17 1995-07-12 三菱化学株式会社 Method for manufacturing water-absorbent composite material
US5160789A (en) * 1989-12-28 1992-11-03 The Procter & Gamble Co. Fibers and pulps for papermaking based on chemical combination of poly(acrylate-co-itaconate), polyol and cellulosic fiber
FR2670516B1 (en) * 1990-12-13 1993-04-09 Hoechst France PROCESS FOR COATING PAPERS AND ITS APPLICATION TO FLEXOGRAPHY.
US5266162A (en) * 1990-12-13 1993-11-30 Societe Francaise Hoechst Process for coating papers and its use in flexographic printing
US5434339A (en) * 1993-03-16 1995-07-18 La Motte; Dennis K. Applying a fluid absorption mat to a floor
CA2175792C (en) * 1993-11-17 2000-10-31 Dean Van Phan Process of making absorbent structures and absorbent structures produced thereby
SG63577A1 (en) * 1993-11-17 1999-03-30 Procter & Gamble Corrugated capillary substrate having selectively disposed discrete parts of osmotic absorbent material
US6022610A (en) * 1993-11-18 2000-02-08 The Procter & Gamble Company Deposition of osmotic absorbent onto a capillary substrate without deleterious interfiber penetration and absorbent structures produced thereby
TW264430B (en) 1993-11-18 1995-12-01 Procter & Gamble
US5709747A (en) * 1994-04-25 1998-01-20 Avgol Nonwoven Industries Coating selective zones of thin webs to change the pervious character thereof, using a cover
US5487942A (en) * 1994-04-28 1996-01-30 Nippon Sanmo Sensyoku Co., Ltd. Carboxyl group-modified acrylonitrile fiber and process of producing same
DE69428980D1 (en) * 1994-04-29 2001-12-13 Nippon Sanmo Sensyoku Co Ltd Carboxy group modified cellulose or acrylic fibers and process for making the same
JPH08311290A (en) * 1995-05-23 1996-11-26 Showa Denko Kk Composition for liquid-absorbing material, molding of liquid-absorbing material, and production thereof
US5840403A (en) * 1996-06-14 1998-11-24 The Procter & Gamble Company Multi-elevational tissue paper containing selectively disposed chemical papermaking additive
US6228506B1 (en) 1998-03-16 2001-05-08 Natural Resources Canada Cellulose/polymer composite enthalpy exchanger and method for its manufacture
US6110533A (en) * 1998-03-16 2000-08-29 Her Majesty The Queen In Right Of Canada, As Represented By The Minister Of Natural Resources Polymeric desiccant articles and process for their manufacture
KR100545673B1 (en) * 1998-06-22 2006-05-23 송원산업주식회사 Manufacturing method of porous absorbent resin
AU3192600A (en) * 1999-03-16 2000-10-04 Mitsubishi Chemical Corporation Water-absorbing composite and process for continuously producing the same
US20030101518A1 (en) * 2000-01-18 2003-06-05 Nano-Tex, Llc Hydrophilic finish for fibrous substrates
US6645256B2 (en) 2001-04-04 2003-11-11 Healthtex Apparel Corp. Polymer grafted cotton
US6645255B2 (en) 2001-04-04 2003-11-11 Healthtex Apparel Corp. Polymer-grafted stretchable cotton
US6638319B2 (en) 2001-04-04 2003-10-28 Healthtex Apparel Corp. Polymer for printed cotton
US7135209B2 (en) * 2001-06-08 2006-11-14 Basf Aktiengesellschaft Water soluble radiation activatable polymer resins
US7142242B2 (en) 2001-10-16 2006-11-28 Victor Company Of Japan, Ltd. Prismatic image forming optical device adapted for miniaturization
TWI239340B (en) * 2001-12-06 2005-09-11 Nippon Catalytic Chem Ind Process for production of water-soluble (meth)acrylic polymers, water-soluble (meth)acrylic polymers, and use thereof
US20060090648A1 (en) * 2002-05-01 2006-05-04 Soane David S Hydrophilic finish for fibrous substrates
US20040143030A1 (en) * 2002-09-11 2004-07-22 Fumiyoshi Ikkai Method of producing synthetic polymer gel and said gel
US7338625B2 (en) 2002-09-18 2008-03-04 Kimberly-Clark Worldwide, Inc. Methods of restoring elasticity after stiffening treatments
US20040204554A1 (en) * 2003-04-09 2004-10-14 Ko Young Chan Process for making a multifunctional superabsorbent polymer
EP1640384A4 (en) * 2003-05-19 2006-08-02 Mitsubishi Chem Corp Process for production of water-absorbing composites
CN101511318B (en) 2006-09-14 2011-09-07 埃伯索贝斯特公司 Fluid absorption pad
KR101382030B1 (en) * 2011-08-04 2014-04-14 코오롱인더스트리 주식회사 Superabsorbent Yarn and Method for Manufacturing The Same
DE102013003755A1 (en) * 2013-03-06 2014-09-11 Carl Freudenberg Kg ventilation insert
BR112016009986B1 (en) 2013-11-07 2020-12-29 Bsn Medical Gmbh medical plaster and its use
US9780347B2 (en) * 2015-03-09 2017-10-03 Johns Manville Acid resistant glass mats that include binders with hydrophilic agents
KR101867430B1 (en) 2016-08-05 2018-06-15 한국원자력연구원 Fabrication method of functional fabrics
JP7032076B2 (en) * 2017-08-09 2022-03-08 帝人フロンティア株式会社 Fiber structure and its manufacturing method
CN112973397B (en) * 2021-03-30 2023-03-10 江苏河海乾诚智能科技有限公司 Preparation method of safe and efficient humidity-adjusting material

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1123283B (en) * 1959-08-04 1962-02-08 Bayer Ag Process for the antistatic finishing of textiles
NL281050A (en) * 1961-07-20
US3434870A (en) * 1965-02-17 1969-03-25 Cotton Producers Inst Treating cellulosic textiles
US4008353A (en) * 1974-03-13 1977-02-15 The Dow Chemical Company Water swellable articles
US3995998A (en) * 1974-08-28 1976-12-07 The United States Of America As Represented By The Secretary Of Agriculture Method of polymerizing and fixing carboxyl-containing vinyl monomers in high conversion on fibrous substrates
US4072784A (en) * 1974-08-28 1978-02-07 The United States Of America As Represented By The Secretary Of Agriculture Fixation of multivalent metal salts of carboxyl-containing vinyl monomers on fibrous substrates
US4304564A (en) * 1980-05-05 1981-12-08 The United States Of America As Represented By The Secretary Of Agriculture Wrinkle-resistant and durable-press cotton-containing fabric by treatment with acrylamide and glyoxal
GR75732B (en) * 1980-08-25 1984-08-02 Johnson & Johnson
JPS6018690B2 (en) * 1981-12-30 1985-05-11 住友精化株式会社 Method for improving water absorbency of water absorbent resin
JPS6155202A (en) * 1984-08-25 1986-03-19 マルハ株式会社 Paper and cloth article provided with high water absorbability
JPS61166809A (en) * 1985-01-19 1986-07-28 Hayashikane Zosen Kk Highly water-absorbing powder
JPS61275355A (en) * 1985-05-29 1986-12-05 Kao Corp Absorptive article
JP3264863B2 (en) * 1997-06-19 2002-03-11 株式会社内外 Universal connection device

Also Published As

Publication number Publication date
CA1302806C (en) 1992-06-09
EP0262405A3 (en) 1990-01-24
AU600024B2 (en) 1990-08-02
US4865886A (en) 1989-09-12
EP0262405A2 (en) 1988-04-06
DE3774232D1 (en) 1991-12-05
JPS6357617A (en) 1988-03-12
KR950013035B1 (en) 1995-10-24
KR880002902A (en) 1988-05-12
ES2027267T3 (en) 1992-06-01
EP0262405B1 (en) 1991-10-30
TW255900B (en) 1995-09-01
AU7766187A (en) 1988-03-03

Similar Documents

Publication Publication Date Title
JPH0780970B2 (en) Method for manufacturing water-absorbent composite material
JPH0647626B2 (en) Method for manufacturing water-absorbent composite material
JPH0764896B2 (en) Method for manufacturing water-absorbent composite material
US4835020A (en) Process for preparation of water absorptive composite material
JPH0967403A (en) Water absorptive composite material and its production
JPH07121975B2 (en) Method for producing water-absorbent composite
JPH07119264B2 (en) Method for producing water-absorbent composite
JPH0689065B2 (en) Method for producing water-absorbent composite
JPH07121976B2 (en) Method for producing water-absorbent composite
JPH0621126B2 (en) Method for producing absorbent composite
JPH07119262B2 (en) Method for producing water-absorbent composite
JPH0774277B2 (en) Method for producing water-absorbent composite
JPH0689077B2 (en) Method for producing water-absorbent composite
JPS62133183A (en) Production of water absorbable composite
JPH07119263B2 (en) Method for producing water-absorbent composite
JPS62225507A (en) Production of water-absorbing composite
JPS62133184A (en) Production of water absorbable composite
JPH03287870A (en) Production of water-absorptive composite
JPS6222810A (en) Production of water-absorptive composite
JPS6297979A (en) Production of water absorbable composite
JPS6297978A (en) Production of water absorbable composite

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term